|Número de publicación||US7343973 B2|
|Tipo de publicación||Concesión|
|Número de solicitud||US 11/056,635|
|Fecha de publicación||18 Mar 2008|
|Fecha de presentación||11 Feb 2005|
|Fecha de prioridad||8 Ene 2002|
|También publicado como||US20060089266|
|Número de publicación||056635, 11056635, US 7343973 B2, US 7343973B2, US-B2-7343973, US7343973 B2, US7343973B2|
|Inventores||Ronald G. Dusterhoft, Harvey J. Fitzpatrick, David Adams, Walter F. Glover, Philip D. Nguyen|
|Cesionario original||Halliburton Energy Services, Inc.|
|Exportar cita||BiBTeX, EndNote, RefMan|
|Citas de patentes (100), Otras citas (49), Citada por (25), Clasificaciones (18), Eventos legales (3)|
|Enlaces externos: USPTO, Cesión de USPTO, Espacenet|
This application is a continuation-in-part of U.S. application Ser. No. 10/972,648 filed on Oct. 25, 2004 now U.S. Pat. No. 7, 267,171 and titled “Methods and Compositions for Stabilizing the Surface of a Subterranean Formation,” which is a continuation-in-part of U.S. application Ser. No. 10/407,643 filed on Apr. 4, 2003 and issued as U.S. Pat. No. 6,962,200, which is a continuation-in-part of U.S. application Ser. No. 10/260,888 filed on Sep. 30, 2002 and issued as U.S. Pat. No. 6,725,931, which is a continuation-in-part of U.S. application Ser. No. 10/183,200 filed Jun. 26, 2002 and issued as U.S. Pat. No. 6,729,404, which is a continuation-in-part of 10/163,183 filed Jun. 4, 2002, now abandoned, which is a continuation-in-part of U.S. application Ser. No. 10/041,142 filed on Jan. 8, 2002 and issued as U.S. Pat. No. 6,668,926.
The present invention relates to methods and compositions of stabilizing a surface within a subterranean formation or fracture. More particularly, the present invention relates to stabilizing surfaces within a subterranean formation or fracture using lightweight proppant coated with an adhesive substance.
Hydrocarbon-producing wells are often stimulated by hydraulic fracturing treatments. In hydraulic fracturing treatments, a viscous fracturing fluid, which also functions as a carrier fluid, is pumped into a producing zone at a rate and pressure such that one or more fractures are formed in the zone. Typically, particulates, such as graded sand, suspended in a portion of the fracturing fluid are then deposited in the fractures when the fracturing fluid is converted to a thin fluid to be returned to the surface. These particulate solids, or “proppant particulates,” serve to prevent the fractures from fully closing so that conductive channels are formed through which produced hydrocarbons can flow.
To prevent the subsequent flowback of proppant and other particulates with the produced fluids, a portion of the proppant introduced into the fractures may be coated with a curable resin or tackifying agent that may facilitate the consolidation of the proppant particles in the fracture. The partially closed fractures apply pressure to the coated proppant particulates whereby the particulates are forced into contact with each other while the resin or tackifying agent enhances the grain-to-grain contact between individual proppant particles. The action of the pressure and the resin or tackifying agent bring about the consolidation of the proppant particles into a permeable mass having compressive and tensile strength, while allowing small amounts of deformation at the surface of the proppant packs to reduce the effects of point loading and/or to reduce proppant crushing.
Most proppant pack treatments have focused on consolidating the proppant pack itself, neglecting the importance of the interaction between the mechanical properties of the subterranean formation in which the proppant pack is placed and the proppant pack. These interactions can have a dramatic effect on overall fracture conductivity. In particular, under high stress and/or high flow conditions, formation material can intrude into the proppant pack, potentially damaging the pack. The intrusion of formation material into the proppant pack can also increase the amount of point loading and/or proppant crushing experienced by the proppant pack. These phenomena can reduce the overall conductivity of the propped fracture and/or the permeability of the proppant pack, which may negatively affect the production of the well.
The present invention relates to methods and compositions of stabilizing a surface within a subterranean formation or fracture. More particularly, the present invention relates to stabilizing surfaces within a subterranean formation or fracture using lightweight proppant coated with an adhesive substance.
One embodiment of the present invention provides a method of treating a subterranean formation comprising: providing a treatment fluid comprising lightweight proppant at least partially coated with an adhesive substance; introducing the treatment fluid into a portion of a subterranean formation; depositing at least a portion of the lightweight proppant in the portion of the subterranean formation; allowing at least a portion of the lightweight proppant in the subterranean formation to form a particulate pack; and, allowing at least a portion of the adhesive substance to migrate from the lightweight particulates to a surface within the portion of the subterranean formation.
Another embodiment of the present invention provides a method of stabilizing a surface within a subterranean fracture, comprising: providing a treatment fluid comprising lightweight proppant at least partially coated with an adhesive substance; introducing the treatment fluid into the subterranean fracture; depositing the lightweight proppant in the subterranean fracture so as to form a proppant pack; and, allowing at least a portion of the adhesive substance to migrate from the lightweight proppant to a surface within the fracture.
Another embodiment of the present invention provides a method of fracturing a subterranean formation, comprising: providing a fracturing fluid comprising lightweight particulates at least partially coated with an adhesive substance; introducing the fracturing fluid into a subterranean formation at a pressure sufficient to create or enhance at least one fracture therein; depositing at least a portion of the lightweight particulates in the at least one fracture having at least one fracture face; and, allowing at least a portion of the adhesive substance to migrate from the lightweight particulates to at least one fracture face.
The features and advantages of the present invention will be readily apparent to those skilled in the art upon a reading of the description of the preferred embodiments that follows.
The present invention relates to methods and compositions of stabilizing a surface within a subterranean formation or fracture. More particularly, the present invention relates to stabilizing surfaces within a subterranean formation or fracture using lightweight proppant coated with an adhesive substance.
In accordance with the present invention, lightweight proppant at least partially coated with an adhesive substance may be used to stabilize a surface within a subterranean formation, such as the face of a fracture, perforation tunnel walls, formation face of an open hole completion interval, or the walls of a well bore. As used herein, the term “adhesive substance” refers to a material (such as a resin or tackifier) that is capable of being coated onto a particulate and that at least temporarily exhibits a sticky or tacky character such that the proppant particulates that have adhesive thereon have a tendency to adhere to adjacent surfaces be those surfaces other particulates, fracture faces or subterranean surfaces, or combinations thereof. In the methods of the present invention, the adhesive substance is coated onto lightweight proppant in a flowable (i.e., substantially liquid) form and remains flowable at least until the coated proppant is placed in contact with a surface within the subterranean formation. Once deposited on or near a surface within a subterranean formation, the adhesive substances may migrate from the proppant to the surface where it may then act to at least partially stabilize the surface. This stabilization of the surface may dramatically improve the permeability of a proppant pack placed within a fracture wherein the face has been so stabilized. Furthermore, stabilization of a fracture face may prevent the intrusion of formation material into the proppant pack, minimizing the damage that can occur to the proppant pack under high stress and/or high flow conditions.
Generally, any treatment fluid suitable for use in a subterranean application may be used in accordance with the teachings of the present invention, including water, brine, oil, weighted water, aqueous gels, viscoelastic surfactant gels, oil gels, foams, a gas, an emulsions, and combinations thereof. In embodiments wherein a gas is used as all or part of the treatment fluid, nitrogen, carbon dioxide, or some combination thereof may be preferred. Suitable aqueous gels are generally comprised of water and one or more gelling agents. Suitable emulsions can be comprised of two immiscible liquids such as an aqueous gelled liquid and a liquefied gas, such as carbon dioxide or nitrogen. In exemplary embodiments of the present invention, the treatment fluids are aqueous gels that comprise water, a gelling agent for increasing viscosity, and, optionally, a crosslinking agent for crosslinking the gelling agent to further increase the viscosity of the fluid to form a crosslinked treatment fluid. The increased viscosity of the gelled, or gelled and cross-linked, treatment fluid, inter alia, reduces fluid loss and allows the treatment fluid to transport significant quantities of suspended proppant particles. The water used to form the treatment fluid may be salt water, brine, or any other aqueous liquid that does not adversely react with the other components.
A variety of gelling agents may be used, including hydratable polymers that contain one or more functional groups such as hydroxyl, carboxyl, sulfate, sulfonate, amino, or amide groups. Suitable gelling agents typically comprise polysaccharides, biopolymers, synthetic polymers, or a combination thereof. A variety of gelling agents can be used in conjunction with the methods and compositions of the present invention, including, but not limited to, hydratable polymers that contain one or more functional groups such as hydroxyl, cis-hydroxyl, carboxylic acids, derivatives of carboxylic acids, sulfate, sulfonate, phosphate, phosphonate, amino, or amide. In certain exemplary embodiments, the gelling agents may be polymers comprising polysaccharides, and derivatives thereof, that contain one or more of these monosaccharide units: galactose; mannose; glucoside; glucose; xylose; arabinose; fructose; glucuronic acid; or pyranosyl sulfate. Examples of suitable polymers include, but are not limited to, guar gum and derivatives thereof, such as hydroxypropyl guar and carboxymethylhydroxypropyl guar, and cellulose derivatives, such as hydroxyethyl cellulose. Additionally, synthetic polymers and copolymers that contain the above-mentioned functional groups may be used. Examples of such synthetic polymers include, but are not limited to, polyacrylate, polymethacrylate, polyacrylamide, polyvinyl alcohol, and polyvinylpyrrolidone. In other exemplary embodiments, the gelling agent molecule may be depolymerized. The term “depolymerized,” as used herein, generally refers to a decrease in the molecular weight of the gelling agent molecule. Depolymerized gelling agent molecules are described in U.S. Pat. No. 6,488,091, issued Dec. 3, 2002 to Weaver, et al., the relevant disclosure of which is incorporated herein by reference. Suitable gelling agents generally are present in the viscosified treatment fluids of the present invention in an amount in the range of from about 0.1% to about 5% by weight of the water therein. In certain exemplary embodiments, the gelling agents are present in the viscosified treatment fluids of the present invention in an amount in the range of from about 0.01% to about 2% by weight of the water therein.
In some embodiments the present invention, the density of the treatment fluid may be increased using one or more weighting agents, that is, solid particles that may be suspended in a fluid to increase its density (and thus its particulate carrying ability). In some embodiments such weighting agents may be used in addition to other viscosifying agents (such as guar) and in other embodiments they may be used alone. In some embodiments the chosen weighting agent may confer benefits beyond just increasing the treatment fluid's density. In particular, where a chosen weighting agent is a material that will degrade over time in the treatment fluid or in the fluids present in the subterranean formation being treated, the weighting agent may also act to increase the porosity of a resultant proppant pack. By way of example, when a weighting agent comprising a salt is used in a treatment fluid carrying proppant to form a proppant pack, once the pack is formed the salt may degrade or dissolve over time leaving behind void spaces in the proppant pack. The weighting material may be selected to degrade in the subterranean environment or to remain permanently. As one skilled in the art may recognize, in embodiments wherein it is desirable for the weighting agent to degrade, it may be selected to be water-degradable or oil-degradable depending on the subterranean environment to which the weighting agent will be exposed.
Crosslinking agents may be used to crosslink gelling agent molecules to form crosslinked gelling agents. Crosslinkers typically comprise at least one metal that is capable of crosslinking at least two gelling agent molecules. Examples of suitable crosslinkers include, but are not limited to, zirconium compounds (such as, for example, zirconium lactate, zirconium lactate triethanolamine, zirconium carbonate, zirconium acetylacetonate, zirconium malate, zirconium citrate, and zirconium diisopropylamine lactate); titanium compounds (such as, for example, titanium lactate, titanium malate, titanium citrate, titanium ammonium lactate, titanium triethanolamine, and titanium acetylacetonate); aluminum compounds (such as, for example, aluminum lactate or aluminum citrate); antimony compounds; chromium compounds; iron compounds; copper compounds; zinc compounds; or a combination thereof. An example of a suitable commercially available zirconium-based crosslinker is “CL-24,” available from Halliburton Energy Services, Inc., Duncan, Okla. An example of a suitable commercially available titanium-based crosslinker is “CL-39,” available from Halliburton Energy Services, Inc., Duncan Okla. Suitable crosslinkers generally are present in the viscosified treatment fluids of the present invention in an amount sufficient to provide, inter alia, the desired degree of crosslinking between gelling agent molecules. In certain exemplary embodiments of the present invention, the crosslinkers may be present in an amount in the range from about 0.001% to about 10% by weight of the water in the fracturing fluid. In certain exemplary embodiments of the present invention, the crosslinkers may be present in the viscosified treatment fluids of the present invention in an amount in the range from about 0.01% to about 1% by weight of the water therein. Individuals skilled in the art, with the benefit of this disclosure, will recognize the exact type and amount of crosslinker to use depending on factors such as the specific gelling agent, desired viscosity, and formation conditions.
The gelled or gelled and cross-linked treatment fluids may also include internal delayed gel breakers such as enzymes, oxidizing agents, acid buffers, or temperature-activated gel breakers. The gel breakers cause the viscous treatment fluids to revert to thin fluids that can be produced back to the surface after they have been used to place proppant particulates in subterranean fractures. The gel breaker used is typically present in the treatment fluid in an amount in the range of from about 0.5% to about 10% by weight of the gelling agent. The treatment fluids may also include one or more of a variety of well-known additives, such as gel stabilizers, fluid loss control additives, clay stabilizers, bactericides, and the like.
Any suitable lightweight proppant may be used in accordance with the teachings of the present invention, including lightweight sand, lightweight nut shells, lightweight seed shells, lightweight bauxite materials, lightweight ceramic materials, lightweight glass materials, lightweight polymer beads, lightweight composite particles, lightweight resinous materials, lightweight resinous materials comprising nut shells and/or seed shells, combinations thereof, and the like. As used herein, “lightweight proppant” refers to any proppant having a specific gravity of less than about 2.7. In some embodiments, lightweight proppant particulates of the present invention have a specific gravity from about 0.7 to about 2.7. In other embodiments, lightweight proppant particulates of the present invention have a specific gravity of less than about 2.5. In other embodiments, lightweight proppant particulates of the present invention have a specific gravity of less than about 2.2. In other embodiments, lightweight proppant particulates of the present invention have a specific gravity of less than about 2. In other embodiments, lightweight proppant particulates of the present invention have a specific gravity of less than about 1.7. In other embodiments, lightweight proppant particulates of the present invention have a specific gravity of less than about 1.5. In other embodiments, lightweight proppant particulates of the present invention have a specific gravity of less than about 1.3. In other embodiments, lightweight proppant particulates of the present invention have a specific gravity of less than about 1. Some suitable lightweight proppant particulates are described in U.S. Pat. Nos. 6,632,527, 6,582,819, 6,749,025, 6,364,018, 5,582,250, 5,531,274, 4,969,523, 4,850,430, and 4,733,729, the relevant disclosures of which are hereby incorporated by reference. In particular embodiments of the present invention, the lightweight proppant particulates may be of a size such that formation fines that may migrate with produced fluids are prevented from being produced from the subterranean zone. Generally, the proppant particulates have a size in the range of from about 2 mesh to about 400 mesh, U.S. Sieve Series. In some embodiments of the present invention, the proppant is graded sand having a particulate size in the range of from about 10 mesh to about 70 mesh, U.S. Sieve Series. In particular embodiments, preferred proppant particulate size distribution ranges are one or more of 10-20 mesh, 20-40 mesh, 40-60 mesh, or 50-70 mesh, depending on the particular size and distribution of formation solids to be screened out by the proppant particulates. It should be understood that the term “proppant,” as used in this disclosure, includes all known shapes of materials, including substantially spherical materials, fibrous materials, polygonal materials (such as cubic materials) and mixtures thereof. Moreover, fibrous materials that may or may not be used to bear the pressure of a closed fracture are often included in proppant and gravel treatments to, among other things, increase the conductivity of a resulting pack by forming highly conductive channels.
Generally, the lightweight proppant particulates of the present invention are at least partially coated with an adhesive substance. Any adhesive substance capable of migrating from the surface of the proppant to a surface of the subterranean formation may be used in accordance with the teachings of the present invention. Suitable adhesive substances include, but are not limited to, resins, nonaqueous tackifying agents, aqueous tackifying agents, and silyl-modified polyamides.
Resins suitable for use in the consolidation fluids of the present invention include all resins known in the art that are capable of forming a hardened, consolidated mass. Many such resins are commonly used in subterranean consolidation operations, and some suitable resins include two component epoxy based resins, novolak resins, polyepoxide resins, phenol-aldehyde resins, urea-aldehyde resins, urethane resins, phenolic resins, furan resins, furan/furfuryl alcohol resins, phenolic/latex resins, phenol formaldehyde resins, polyester resins and hybrids and copolymers thereof, polyurethane resins and hybrids and copolymers thereof, acrylate resins, and mixtures thereof. Some suitable resins, such as epoxy resins, may be cured with an internal catalyst or activator so that when pumped down hole, they may be cured using only time and temperature. Other suitable resins, such as furan resins, generally require a time-delayed catalyst or an external catalyst to help activate the polymerization of the resins if the cure temperature is low (i.e., less than 250° F.), but will cure under the effect of time and temperature if the formation temperature is above about 250° F., preferably above about 300° F. It is within the ability of one skilled in the art, with the benefit of this disclosure, to select a suitable resin for use in embodiments of the present invention and to determine whether a catalyst is required to trigger curing.
Selection of a suitable resin may be affected by the temperature of the subterranean formation to which the fluid will be introduced. By way of example, for subterranean formations having a bottom hole static temperature (BHST) ranging from about 60° F. to about 250° F., two-component epoxy-based resins comprising a hardenable resin component and a hardening agent component containing specific hardening agents may be preferred. For subterranean formations having a BHST ranging from about 300° F. to about 600° F., a furan-based resin may be preferred. For subterranean formations having a BHST ranging from about 200° F. to about 400° F., either a phenolic-based resin or a one-component HT epoxy-based resin may be suitable. For subterranean formations having a BHST of at least about 175° F., a phenol/phenol formaldehyde/furfuryl alcohol resin may also be suitable.
Any solvent that is compatible with the chosen resin and achieves the desired viscosity effect is suitable for use in the present invention. Some preferred solvents are those having high flash points (e.g., about 125° F.) because of, among other things, environmental and safety concerns; such solvents include butyl lactate, butylglycidyl ether, dipropylene glycol methyl ether, dipropylene glycol dimethyl ether, dimethyl formamide, diethyleneglycol methyl ether, ethyleneglycol butyl ether, diethyleneglycol butyl ether, propylene carbonate, methanol, butyl alcohol, d'limonene, fatty acid methyl esters, and combinations thereof. Other preferred solvents include aqueous dissolvable solvents such as, methanol, isopropanol, butanol, glycol ether solvents, and combinations thereof. Suitable glycol ether solvents include, but are not limited to, diethylene glycol methyl ether, dipropylene glycol methyl ether, 2-butoxy ethanol, ethers of a C2 to C6 dihydric alkanol containing at least one C1 to C6 alkyl group, mono ethers of dihydric alkanols, methoxypropanol, butoxyethanol, hexoxyethanol, and isomers thereof. Selection of an appropriate solvent is dependent on the resin chosen and is within the ability of one skilled in the art with the benefit of this disclosure.
Tackifying agents suitable for use in the present invention include nonaqueous tackifying agents, aqueous tackifying agents, and silyl-modified polyamides. In addition to encouraging the proppant particulates to form aggregates, the use of a tackifying agent may yield a propped fracture that experiences very little or no undesirable proppant flow back. The application of a tackifying agent to the proppant particulates may aid in the formation of aggregates that increase the ability of a smaller amount of proppant particulates to effectively hold open a fracture for production. Tackifying agents may be applied on-the-fly, applying the adhesive substance to the proppant particulate at the well site, directly prior to pumping the fluid-proppant mixture into the well bore.
One type of tackifying agent suitable for use in the present invention is a nonaqueous tackifying agent. A particularly preferred group of tackifying agents comprise polyamides that are liquids or in solution at the temperature of the subterranean formation such that they are, by themselves, nonhardening when introduced into the subterranean formation. A particularly preferred product is a condensation reaction product comprised of commercially available polyacids and a polyamine. Such commercial products include compounds such as mixtures of C36 dibasic acids containing some trimer and higher oligomers and also small amounts of monomer acids that are reacted with polyamines. Other polyacids include trimer acids, synthetic acids produced from fatty acids, maleic anhydride, acrylic acid, and the like. Such acid compounds are commercially available from companies such as Witco Corporation, Union Camp, Chemtall, and Emery Industries. The reaction products are available from, for example, Champion Technologies, Inc. and Witco Corporation. Additional compounds which may be used as nonaqueous tackifying compounds include liquids and solutions of, for example, polyesters, polycarbonates and polycarbamates, natural resins such as shellac and the like. Other suitable nonaqueous tackifying agents are described in U.S. Pat. No. 5,853,048 issued to Weaver, et al. and U.S. Pat. No. 5,833,000 issued to Weaver, et al., the relevant disclosures of which are herein incorporated by reference.
Nonaqueous tackifying agents suitable for use in the present invention may be either used such that they form non-hardening coating or they may be combined with a multifunctional material capable of reacting with the nonaqueous tackifying agent to form a hardened coating. A “hardened coating,” as used herein, means that the reaction of the tackifying compound with the multifunctional material will result in a substantially non-flowable reaction product that exhibits a higher compressive strength in a consolidated agglomerate than the tackifying compound alone with the particulates. In this instance, the nonaqueous tackifying agent may function similarly to a hardenable resin. Multifunctional materials suitable for use in the present invention include, but are not limited to, aldehydes such as formaldehyde, dialdehydes such as glutaraldehyde, hemiacetals or aldehyde-releasing compounds, diacid halides, dihalides such as dichlorides and dibromides, polyacid anhydrides such as citric acid, epoxides, furfuraldehyde, glutaraldehyde or aldehyde condensates and the like, and combinations thereof. In some embodiments of the present invention, the multifunctional material may be mixed with the tackifying compound in an amount of from about 0.01% to about 50% by weight of the tackifying compound to effect formation of the reaction product. In some preferable embodiments, the compound is present in an amount of from about 0.5% to about 1% by weight of the tackifying compound. Suitable multifunctional materials are described in U.S. Pat. No. 5,839,510, issued to Weaver, et al., the relevant disclosure of which is herein incorporated by reference.
Solvents suitable for use with the nonaqueous tackifying agents of the present invention include any solvent that is compatible with the nonaqueous tackifying agent and achieves the desired viscosity effect. The solvents that can be used in the present invention preferably include those having high flash points (most preferably above about 125° F.). Examples of solvents suitable for use in the present invention include, but are not limited to, butylglycidyl ether, dipropylene glycol methyl ether, butyl bottom alcohol, dipropylene glycol dimethyl ether, diethyleneglycol methyl ether, ethyleneglycol butyl ether, methanol, butyl alcohol, isopropyl alcohol, diethyleneglycol butyl ether, propylene carbonate, d'limonene, 2-butoxy ethanol, butyl acetate, furfuryl acetate, butyl lactate, dimethyl sulfoxide, dimethyl formamide, fatty acid methyl esters, and combinations thereof. It is within the ability of one skilled in the art, with the benefit of this disclosure, to determine whether a solvent is needed to achieve a viscosity suitable to the subterranean conditions and, if so, how much.
Aqueous tackifyier agents suitable for use in the present invention are not significantly tacky when placed onto a particulate, but are capable of being “activated” (that is, destabilized, coalesced, and/or reacted) to transform the compound into a sticky, tackifying compound at a desirable time. Such activation may occur before, during, or after the aqueous tackifier agent is placed in the subterranean formation. In some embodiments, a pretreatment may be first contacted with the surface of a particulate to prepare it to be coated with an aqueous tackifier agent. Suitable aqueous tackifying agents are generally charged polymers that comprise compounds that, when in an aqueous solvent or solution, will form a nonhardening coating (by itself or with an activator) and, when placed on a particulate, will increase the continuous critical resuspension velocity of the particulate when contacted by a stream of water. The aqueous tackifier agent may enhance the grain-to-grain contact between the individual particulates within the formation (be they proppant particulates, formation fines, or other particulates), helping bring about the consolidation of the particulates into a cohesive, flexible, and permeable mass.
Examples of aqueous tackifier agents suitable for use in the present invention include, but are not limited to, acrylic acid polymers, acrylic acid ester polymers, acrylic acid derivative polymers, acrylic acid homopolymers, acrylic acid ester homopolymers (such as poly(methyl acrylate), poly (butyl acrylate), and poly(2-ethylhexyl acrylate)), acrylic acid ester co-polymers, methacrylic acid derivative polymers, methacrylic acid homopolymers, methacrylic acid ester homopolymers (such as poly(methyl methacrylate), poly(butyl methacrylate), and poly(2-ethylhexyl methacryate)), acrylamido-methyl-propane sulfonate polymers, acrylamido-methyl-propane sulfonate derivative polymers, acrylamido-methyl-propane sulfonate co-polymers, and acrylic acid/acrylamido-methyl-propane sulfonate co-polymers, and combinations thereof. Methods of determining suitable aqueous tackifier agents and additional disclosure on aqueous tackifier agents can be found in U.S. patent application Ser. No. 10/864,061, and filed Jun. 9, 2004, and U.S. patent application Ser. No. 10/864,618, and filed Jun. 9, 2004 the relevant disclosures of which are hereby incorporated by reference.
Another tackifying agent suitable for in the present invention is a silyl-modified polyamide compound that may be described as a substantially self-hardening composition that is capable of at least partially adhering to particulates in the unhardened state, and that is further capable of self-hardening itself to a substantially non-tacky state to which individual particulates such as formation fines will not adhere, for example, in formation or proppant pack pore throats. Such silyl-modified polyamides may be based, for example, on the reaction product of a silating compound with a polyamide or a mixture of polyamides. The polyamide or mixture of polyamides may be one or more polyamide intermediate compounds obtained, for example, from the reaction of a polyacid (e.g., diacid or higher) with a polyamine (e.g., diamine or higher) to form a polyamide polymer with the elimination of water. Other suitable silyl-modified polyamides and methods of making such compounds are described in U.S. Pat. No. 6,439,309, issued to Matherly, et al., the relevant disclosure of which is herein incorporated by reference.
In particular embodiments of the present invention, proppant particulates are coated with the adhesive substance, typically on-the-fly, the coated proppant particulates are suspended in the fracturing fluid, also typically on-the-fly, and the resulting adhesive substance-coated proppant particles are placed in one or more fractures formed in a subterranean zone. The term “on-the-fly” is used herein to mean that a flowing stream is continuously introduced into another flowing stream so that the streams are combined and mixed while continuing to flow as a single stream as part of an ongoing treatment. Forming an adhesive substance, coating the proppant particles with the adhesive substance, and mixing the adhesive substance-coated proppant particles with the fracturing fluid may be typically performed on-the-fly. Such mixing can also be described as “real-time” mixing. As is well understood by those skilled in the art, such mixing may also be accomplished by batch or partial batch mixing. One benefit of on-the-fly mixing over batch or partial batch mixing, however, involves reducing waste of the adhesive substance and any components the adhesive substance may have. For example, in adhesive substances comprising a hardenable resin component and a hardening agent component, once the hardenable resin component and hardening agent component are mixed, the mixture must be used within a short time frame or the resin will cure and the mixture will no longer be pumpable as a result of increase in its viscosity. Thus, if the components are mixed and then circumstances dictate that the well operation be stopped or postponed, the mixed components may quickly become unusable. By having the ability to rapidly shut down the mixing of the adhesive substance components on-the-fly, this unnecessary waste can be avoided, resulting in, among other things, increased efficiency and cost savings.
As mentioned above, during the time that the hardenable resin component and the hardening agent component are mixed and coated on the proppant particulates, the rate of addition of the hardening agent component can be varied while the rate of addition of the hardenable resin component is held constant. Stated another way, in addition to varying whether or not the proppant particulates are coated at all, the volume ratio of the adhesive substance components on those particulates that are coated may be varied as well. This volume ratio may be varied to obtain a desired level of consolidation or toughness for the proppant pack. For example, in adhesive substances comprising a hardening agent component and a hardenable resin component, by increasing the volume ratio of the hardening agent component to the hardenable resin component, the proppant pack may possess a more elastic structure as compared to that when using a reduced volume ratio of the hardening agent component to the hardenable resin component. It should be within the ability of one of ordinary skill in the art, with the benefit of this disclosure, to determine the suitable ratio of components to meet the desired goals.
Once the adhesive substance-coated proppant particulate is deposited into the subterranean fracture, at least a portion of the adhesive substance tends to migrate from the surface of the proppant to a surface with the abutting subterranean formation. This migration is thought to be possible, in part, because the adhesive substance is coated on the proppant particulates in a flowable form and remains flowable at least until the coated proppant particulates are placed in contact with a surface within the subterranean formation. Generally, at least a portion of the resin on the proppant particulates in contact with the fracture face migrates from the proppant to the fracture face through one or more forms of mass transfer (e.g., capillary action, diffusion, adhesion). For example, the adhesive substance may migrate onto the fracture face as a result of the capillary action of formation sand that causes the resin to spread, smear, and/or coat onto the formation grains. This migration of the adhesive substance from the proppant particulates to the fracture face results in stabilization of fracture face, thus mitigating the movement or migration of formation materials, and allowing the conductivity of propped fracture to be maintained under low stress conditions. Under high stress conditions and/or high flow rate conditions, the amount of formation material intruding into the proppant pack may also be reduced.
Even under extreme stress conditions where the proppant particulate crushes, the fracture stabilization provided by particular embodiments of the present invention may also be beneficial. Typically under extreme stress conditions, the use of uncoated proppant particulates has resulted in excessive amounts of formation fines migrating into the pore spaces of the proppant pack. However, the stabilization provided by particular embodiments of the present invention may reduce the amount of formation fines migrating and penetrating into the proppant pack, helping to keep the pore spaces between the proppant grains from being plugged by the formation particulate, and to maintain the flow path and the conductivity of the propped fracture.
Adhesive substance-coated proppant may provide some advantages as compared to uncoated proppant. Such advantages include, among other things, providing a stable, consolidated, and permeable pack able to at least partially withstand the effects of stress cycling and prevent proppant from flowing out of the fracture during production of the well; allowing fines or fine fragments generated from crushed proppant as a result of being exposed to high closure stresses of closing fracture to be confined or entrapped inside the layer of adhesive substance encapsulating the proppant, so they cannot disperse and migrate within the proppant pack; stabilizing the formation materials along the fracture face to keep them from invading into and migrating in the proppant pack, causing pore spaces to be plugged; and increasing the effective contact area between the proppant particulates and the fracture face through accumulation of the resin at the contact points, which may reduce the point load stresses applied as the fracture closes and may thus reduce the amount of formation embedment or intrusion into the proppant pack. The stabilized region created around the points of contact between the proppant grains and the formation face serves to increase the effective area of contact. As a result, there may be a reduction in point loading forces between the proppant and on the formation face helping to reduce deformation of the fracture face or embedment of the proppant into the formation face due to the very high point loads that are seen at the initial points of contact. Stabilization of the formation face and creation of increased contact area may also help disperse the stress load and reduce the amount of embedment of the proppant into the formation face. The result of this may be increased fracture width and increased effective porosity in the proppant pack which may, in turn, result in higher permeability and fracture conductivity.
To facilitate a better understanding of the present invention, the following examples of preferred embodiments are given. In no way should the following examples be read to limit or define the scope of the invention.
Six sets of experiments were performed to evaluate three different types of proppant particulates along with a two-component high temperature epoxy resin system as used in a fracturing operation. In each case, the resin was used at 3% by weight of proppant particulates. The proppant particulate types included 20/40 bauxite (known to handle up to about 12,000 psi without substantial crushing), 18/40 intermediate strength proppant (ISP) (known to handle up to about 8,000 psi without substantial crushing), and 20/40 economical lightweight proppant (ELP) (known to handle up to about 6,000 psi without substantial crushing). The test temperature was steady at 250° F. for all tests. Stress was increased over a period of several days from 2,000 psi to 12,000 psi, allowing measurements to be taken at each condition. A baseline test of uncoated proppant particulates was performed for each material, and each type of proppant particulates was tested with a liquid coated resin (LCR) that would cure over time to form a hard coating and a strong mechanical bond between the proppant grains.
The effects of the closure stresses and flow rates on resin-treated proppant were evaluated with an API-linear conductivity cell. Each proppant sample was placed between the two core slabs within the test cell. The proppant particulates were leveled with a blade device inside the cell before being sandwiched between the core wafers to form a cell assembly. The cell was staked to within 0.002 inches from top to bottom and positioned between the platens of a Dake Press. Each cell was made a part of the three-cell evaluation stack, which included control (i.e., uncoated) proppant particulates and LCR-treated proppant particulates.
To measure conductivity, the test cell was loaded with the appropriate proppant pack placed between Ohio sandstone wafers and placed into the press where closure stress and temperature were applied to the specified test conditions. Pressure was increased to 500 psi, and the system was evacuated and saturated with 2% KCl at 70° F.-75° F. Once saturated, the closure pressure was increased to 1,000 psi, at a rate of 100 psi/min.
Conductivity was then measured with a flow through the proppant pack. The flow rate pressure differential and average width were measured at each pressure to calculate the conductivity and permeability. Five measurements were taken and averaged to arrive at each reported conductivity. Flow rate was measured with a Liquiflow meter calibrated with a Mettler balance to 0.01 ml/min. Darcy's Law was used for the calculations to determine the conductivity and permeability.
The test temperature was then increased to 250° F. and allowed to equilibrate. The temperature was maintained at 250° F. for 12 hours before increasing the closure stress. The conductivity and permeability of the proppant were then determined at 1,000 psi and 250° F. The closure stress was then increased at a rate of 100 psi/min to the next closure stress, and conductivity and permeability measurements were taken as described above.
The conductivity and permeability of each proppant pack was continuously monitored at 2,000 psi and 250° F. for a minimum of 25 to 30 hours. Following this time period, a high-velocity, non-Darcy gas evaluation was performed by increasing the gas rate to an equipment maximum of about 290 standard liters per minute (SLM) and flowing until pressure differential flat lines (dry state) were obtained. The flow rate was then decreased, stopping at selected intermittent rates, until 30 to 35 SLM was achieved. A secondary calibrated Flow Prover monitored the gas flow rate at the exit of the test cell for the calculation of the gas flow rate. Zeros were rechecked, and the rate was increased back to the previous highest flow rate and the down-rate ramp repeated. As closure stresses increased, the highest velocity was limited by imposing a maximum pressure drop limit of 50 psi/5 inches for the pressure differential (and/or maximum equipment flowing pressure was obtained versus flow rate). Following each gas evaluation of the test cells at 2,000 psi closure stresses, 2% KCl was re-introduced into the proppant pack and the cell was de-gassed before a final measurement of conductivity was obtained.
The conductivity and permeability of the proppant packs were also measured at closure stresses of 4,000, 6,000, 8,000, 10,000, and 12,000 psi. In several tests, steel plates were used to encase the proppant pack to help differentiate the effects of curable resin in controlling fines that have been generated from crushed proppant or from fines that have been introduced from the Ohio core wafers.
For all three proppants, there was a significant increase in fracture conductivity and proppant pack permeability for the LCR-coated proppants versus the uncoated proppants. The improvement in fracture conductivity and proppant pack permeability was pronounced under the lower stress conditions. Under lower stress conditions, the LCR-coated proppants showed a near-parallel trend to the uncoated proppants, essentially showing that the proppant pack permeability and fracture conductivity of the LCR-coated proppants were consistently higher than those of the uncoated proppants. In all cases, there was a stress at which the conductivity of the LCR-coated proppants began to converge with the uncoated proppant baseline conductivity/proppant pack permeability. The point at which this convergence initiated was different for each type of proppant particulate.
The measured cell width, which corresponds closely to the width of the proppant pack, showed trends nearly identical to those seen in the proppant pack permeability and fracture conductivity. This suggests that there is greater porosity in the cells with the coated proppants as opposed to the ones with uncoated proppants.
A number of observations were made upon visual inspection of the proppant packs during disassembly of the conductivity test equipment. In all cases, there was evidence of formation material penetrating into the proppant pack. For all three proppants, the amount of formation material that appeared to be filling pore spaces in the proppant pack was much greater for the uncoated proppants. The coated proppants showed much less formation intrusion and much less formation material filling the porosity of the proppant pack. In the bauxite tests, it was difficult to make any judgment regarding the quantity of crushed proppant in the individual tests. For ISP and ELP, it was possible to detect significant variation. In these cases, LCR-coated proppants showed a much more stable interface at the formation-proppant interface, and severe proppant crushing in the center of the proppant pack. The uncoated proppants showed deeper formation intrusions and much less crushed proppant in the pack. It also appeared that the intrusion of formation fines into the proppant pack reduced the point loading on the individual proppant grains, thus reducing the amount of crushing.
With the LCR-coated proppants, there was evidence of a much more stable interface created between the proppant and formation material. The result of this behavior seemed to be an increase in the point loading between proppant grains. As a result, there was more proppant crushing when the cell was placed under extreme stress conditions for a given proppant. This suggests that stabilizing the interface between the proppant and formation material provided a means to achieve the maximum benefit from a given proppant and the effects of formation intrusion were dramatically reduced.
Visual inspection of the proppant face with the formation face removed show that the liquid resin actually accumulated slightly at the interface between the proppant particulates and the formation face. In the case of resin material, a thin layer of formation material actually appeared to be consolidated by resin material that had been drawn from the proppant to the formation, helping to create a stable interface. It also appeared that liquid resin would cure to form a rigid interface where puddle points around each individual proppant grain consolidated from small quantities of resin are drawn by capillary forces and surface effects.
Therefore, the present invention is well adapted to attain the ends and advantages mentioned as well as those that are inherent therein. While numerous changes may be made by those skilled in the art, such changes are encompassed within the spirit of this invention as defined by the appended claims.
|Patente citada||Fecha de presentación||Fecha de publicación||Solicitante||Título|
|US2238671||9 Feb 1940||15 Abr 1941||Du Pont||Method of treating wells|
|US2703316||5 Jun 1951||1 Mar 1955||Du Pont||Polymers of high melting lactide|
|US2869642||14 Sep 1954||20 Ene 1959||Texas Co||Method of treating subsurface formations|
|US3047067||8 Sep 1958||31 Jul 1962||Jersey Prod Res Co||Sand consolidation method|
|US3123138||23 Ago 1962||3 Mar 1964||robichaux|
|US3176768||27 Jul 1964||6 Abr 1965||California Research Corp||Sand consolidation|
|US3199590||25 Feb 1963||10 Ago 1965||Halliburton Co||Method of consolidating incompetent sands and composition therefor|
|US3272650||21 Feb 1963||13 Sep 1966||Union Carbide Corp||Process for cleaning conduits|
|US3297086||30 Mar 1962||10 Ene 1967||Exxon Production Research Co||Sand consolidation method|
|US3308885||28 Dic 1965||14 Mar 1967||Union Oil Co||Treatment of subsurface hydrocarbon fluid-bearing formations to reduce water production therefrom|
|US3316965||5 Ago 1963||2 May 1967||Union Oil Co||Material and process for treating subterranean formations|
|US3375872||2 Dic 1965||2 Abr 1968||Halliburton Co||Method of plugging or sealing formations with acidic silicic acid solution|
|US3404735||1 Nov 1966||8 Oct 1968||Halliburton Co||Sand control method|
|US3415320||9 Feb 1967||10 Dic 1968||Halliburton Co||Method of treating clay-containing earth formations|
|US3492147||22 Oct 1964||27 Ene 1970||Halliburton Co||Method of coating particulate solids with an infusible resin|
|US3659651||17 Ago 1970||2 May 1972||Exxon Production Research Co||Hydraulic fracturing using reinforced resin pellets|
|US3681287||3 Mar 1971||1 Ago 1972||Quaker Oats Co||Siliceous materials bound with resin containing organosilane coupling agent|
|US3754598||8 Nov 1971||28 Ago 1973||Phillips Petroleum Co||Method for producing a hydrocarbon-containing formation|
|US3765804||23 Ene 1967||16 Oct 1973||Brandon O||Apparatus for producing variable high frequency vibrations in a liquid medium|
|US3768564||26 Abr 1971||30 Oct 1973||Halliburton Co||Method of fracture acidizing a well formation|
|US3784585||21 Oct 1971||8 Ene 1974||American Cyanamid Co||Water-degradable resins containing recurring,contiguous,polymerized glycolide units and process for preparing same|
|US3819525||21 Ago 1972||25 Jun 1974||Avon Prod Inc||Cosmetic cleansing preparation|
|US3828854||30 Oct 1973||13 Ago 1974||Shell Oil Co||Dissolving siliceous materials with self-acidifying liquid|
|US3842911||9 Abr 1973||22 Oct 1974||Halliburton Co||Method of fracture acidizing a well formation|
|US3854533||24 Oct 1973||17 Dic 1974||Dow Chemical Co||Method for forming a consolidated gravel pack in a subterranean formation|
|US3857444||2 Feb 1973||31 Dic 1974||Dow Chemical Co||Method for forming a consolidated gravel pack in a subterranean formation|
|US3863709||20 Dic 1973||4 Feb 1975||Mobil Oil Corp||Method of recovering geothermal energy|
|US3868998||15 May 1974||4 Mar 1975||Shell Oil Co||Self-acidifying treating fluid positioning process|
|US3888311||1 Oct 1973||10 Jun 1975||Exxon Production Research Co||Hydraulic fracturing method|
|US3912692||24 Sep 1974||14 Oct 1975||American Cyanamid Co||Process for polymerizing a substantially pure glycolide composition|
|US3948672||26 Sep 1974||6 Abr 1976||Texaco Inc.||Permeable cement composition and method|
|US3955993||26 Sep 1974||11 May 1976||Texaco Inc.||Method and composition for stabilizing incompetent oil-containing formations|
|US3960736||3 Jun 1974||1 Jun 1976||The Dow Chemical Company||Self-breaking viscous aqueous solutions and the use thereof in fracturing subterranean formations|
|US4008763||20 May 1976||22 Feb 1977||Atlantic Richfield Company||Well treatment method|
|US4029148||13 Sep 1976||14 Jun 1977||Atlantic Richfield Company||Well fracturing method|
|US4031958||13 Jun 1975||28 Jun 1977||Union Oil Company Of California||Plugging of water-producing zones in a subterranean formation|
|US4042032||2 Oct 1975||16 Ago 1977||Halliburton Company||Methods of consolidating incompetent subterranean formations using aqueous treating solutions|
|US4070865||10 Mar 1976||31 Ene 1978||Halliburton Company||Method of consolidating porous formations using vinyl polymer sealer with divinylbenzene crosslinker|
|US4074760||1 Nov 1976||21 Feb 1978||The Dow Chemical Company||Method for forming a consolidated gravel pack|
|US4169798||25 Oct 1977||2 Oct 1979||Celanese Corporation||Well-treating compositions|
|US4172066||26 Sep 1977||23 Oct 1979||The Dow Chemical Company||Cross-linked, water-swellable polymer microgels|
|US4245702||7 May 1979||20 Ene 1981||Shell Internationale Research Maatschappij B.V.||Method for forming channels of high fluid conductivity in hard acid-soluble formations|
|US4273187||30 Jul 1979||16 Jun 1981||Texaco Inc.||Petroleum recovery chemical retention prediction technique|
|US4291766||2 Jun 1980||29 Sep 1981||Shell Oil Company||Process for consolidating water-wet sands with an epoxy resin-forming solution|
|US4305463||31 Oct 1970||15 Dic 1981||Oil Trieval Corporation||Oil recovery method and apparatus|
|US4336842||5 Ene 1981||29 Jun 1982||Graham John W||Method of treating wells using resin-coated particles|
|US4352674||6 Ene 1981||5 Oct 1982||Compagnie Francaise Des Petroles||Method of tracing a well drilling mud|
|US4353806||3 Abr 1980||12 Oct 1982||Exxon Research And Engineering Company||Polymer-microemulsion complexes for the enhanced recovery of oil|
|US4387769||10 Ago 1981||14 Jun 1983||Exxon Production Research Co.||Method for reducing the permeability of subterranean formations|
|US4415805||18 Jun 1981||15 Nov 1983||Dresser Industries, Inc.||Method and apparatus for evaluating multiple stage fracturing or earth formations surrounding a borehole|
|US4439489||16 Feb 1982||27 Mar 1984||Acme Resin Corporation||Particles covered with a cured infusible thermoset film and process for their production|
|US4443347||13 May 1983||17 Abr 1984||Baker Oil Tools, Inc.||Proppant charge and method|
|US4460052||10 Ago 1981||17 Jul 1984||Judith Gockel||Prevention of lost circulation of drilling muds|
|US4470915||27 Sep 1982||11 Sep 1984||Halliburton Company||Method and compositions for fracturing subterranean formations|
|US4493875||9 Dic 1983||15 Ene 1985||Minnesota Mining And Manufacturing Company||Proppant for well fractures and method of making same|
|US4494605||11 Dic 1981||22 Ene 1985||Texaco Inc.||Sand control employing halogenated, oil soluble hydrocarbons|
|US4498995||1 Jul 1983||12 Feb 1985||Judith Gockel||Lost circulation drilling fluid|
|US4501328||14 Mar 1983||26 Feb 1985||Mobil Oil Corporation||Method of consolidation of oil bearing sands|
|US4526695||4 Feb 1983||2 Jul 1985||Exxon Production Research Co.||Composition for reducing the permeability of subterranean formations|
|US4527627||28 Jul 1983||9 Jul 1985||Santrol Products, Inc.||Method of acidizing propped fractures|
|US4541489||19 Mar 1984||17 Sep 1985||Phillips Petroleum Company||Method of removing flow-restricting materials from wells|
|US4546012||26 Abr 1984||8 Oct 1985||Carbomedics, Inc.||Level control for a fluidized bed|
|US4553596||28 Jul 1983||19 Nov 1985||Santrol Products, Inc.||Well completion technique|
|US4564459||13 Abr 1984||14 Ene 1986||Baker Oil Tools, Inc.||Proppant charge and method|
|US4572803||30 Jun 1982||25 Feb 1986||Asahi Dow Limited||Organic rare-earth salt phosphor|
|US4649998||2 Jul 1986||17 Mar 1987||Texaco Inc.||Sand consolidation method employing latex|
|US4664819||20 Jun 1985||12 May 1987||Baker Oil Tools, Inc.||Proppant charge and method|
|US4665988||4 Abr 1986||19 May 1987||Halliburton Company||Method of preparation of variable permeability fill material for use in subterranean formations|
|US4669543||23 May 1986||2 Jun 1987||Halliburton Company||Methods and compositions for consolidating solids in subterranean zones|
|US4675140||6 May 1985||23 Jun 1987||Washington University Technology Associates||Method for coating particles or liquid droplets|
|US4683954||5 Sep 1986||4 Ago 1987||Halliburton Company||Composition and method of stimulating subterranean formations|
|US4694905||23 May 1986||22 Sep 1987||Acme Resin Corporation||Precured coated particulate material|
|US4715967||27 Dic 1985||29 Dic 1987||E. I. Du Pont De Nemours And Company||Composition and method for temporarily reducing permeability of subterranean formations|
|US4716964||10 Dic 1986||5 Ene 1988||Exxon Production Research Company||Use of degradable ball sealers to seal casing perforations in well treatment fluid diversion|
|US4733729||4 Feb 1987||29 Mar 1988||Dowell Schlumberger Incorporated||Matched particle/liquid density well packing technique|
|US4739832||24 Dic 1986||26 Abr 1988||Mobil Oil Corporation||Method for improving high impulse fracturing|
|US4785884||28 Ene 1988||22 Nov 1988||Acme Resin Corporation||Consolidation of partially cured resin coated particulate material|
|US4787453||30 Oct 1986||29 Nov 1988||Union Oil Company Of California||Permeability stabilization in subterranean formations containing particulate matter|
|US4789105||16 Abr 1987||6 Dic 1988||Hosokawa Micron Corporation||Particulate material treating apparatus|
|US4796701||30 Jul 1987||10 Ene 1989||Dowell Schlumberger Incorporated||Pyrolytic carbon coating of media improves gravel packing and fracturing capabilities|
|US4797262||3 Jun 1987||10 Ene 1989||Shell Oil Company||Downflow fluidized catalytic cracking system|
|US4800960||18 Dic 1987||31 Ene 1989||Texaco Inc.||Consolidatable gravel pack method|
|US4809783||14 Ene 1988||7 Mar 1989||Halliburton Services||Method of dissolving organic filter cake|
|US4817721||14 Dic 1987||4 Abr 1989||Conoco Inc.||Reducing the permeability of a rock formation|
|US4829100||23 Oct 1987||9 May 1989||Halliburton Company||Continuously forming and transporting consolidatable resin coated particulate materials in aqueous gels|
|US4838352||19 Nov 1987||13 Jun 1989||Dowell Schlumberger Incorporated||Process for plugging subterranean formations|
|US4842072||25 Jul 1988||27 Jun 1989||Texaco Inc.||Sand consolidation methods|
|US4843118||19 Jun 1987||27 Jun 1989||Air Products And Chemicals, Inc.||Acidized fracturing fluids containing high molecular weight poly(vinylamines) for enhanced oil recovery|
|US4848467||16 Feb 1988||18 Jul 1989||Conoco Inc.||Formation fracturing process|
|US4848470||21 Nov 1988||18 Jul 1989||Acme Resin Corporation||Process for removing flow-restricting materials from wells|
|US4850430||4 Feb 1987||25 Jul 1989||Dowell Schlumberger Incorporated||Matched particle/liquid density well packing technique|
|US4886354||6 May 1988||12 Dic 1989||Conoco Inc.||Method and apparatus for measuring crystal formation|
|US4888240||26 Ago 1985||19 Dic 1989||Graham John W||High strength particulates|
|US4895207||19 Dic 1988||23 Ene 1990||Texaco, Inc.||Method and fluid for placing resin coated gravel or sand in a producing oil well|
|US4903770||30 May 1989||27 Feb 1990||Texaco Inc.||Sand consolidation methods|
|US4934456||29 Mar 1989||19 Jun 1990||Phillips Petroleum Company||Method for altering high temperature subterranean formation permeability|
|US4936385||30 Oct 1989||26 Jun 1990||Halliburton Company||Method of particulate consolidation|
|US4942186||2 Mar 1989||17 Jul 1990||Halliburton Company||Continuously forming and transporting consolidatable resin coated particulate materials in aqueous gels|
|US4957165||19 Jun 1989||18 Sep 1990||Conoco Inc.||Well treatment process|
|US20060048943 *||9 Sep 2004||9 Mar 2006||Parker Mark A||High porosity fractures and methods of creating high porosity fractures|
|1||Advances in Polymer Science, vol. 157, "Degradable Aliphatic Polyesters" edited by A.-C. Alberston, 2001.|
|2||Albertsson et al.,"Aliphatic Polyesters: Synthesis, Properties and Applications", Advances in Polymer Science, vol. 57 Degradable Aliphatic Polyesters, 2002.|
|3||Almond, et al, Factors Affecting Proppant Flowback with Resin Coated Proppants, SPE 30096, published 1995, Society of Petroleum Engineers, Inc., pp. 171-186.|
|4||Cantu et al., "Laboratory and Field Evaluation of a Combined Fluid-Loss Control Additive and Gel Breaker for Fracturing Fluids, " SPE 18211, 1990.|
|5||CDX Gas, "What is Coalbed Methane?" CDX, LLC. Available @ www.cdxgas.com/what.html, printed p. 1, undated.|
|6||CDX Gas, CDX Solution, 2003, CDX, LLC, Available @ www.cdxgas.com/solution.html, printed pp. 1-2, undated.|
|7||Chelating Agents, Encyclopedia of Chemical Technology, vol. 5 (764-795), undated.|
|8||Dechy-Cabaret et al., "Controlled Ring-Operated Polymerization of Lactide and Glycolide" American Chemical Society, Chemical Reviews, A-Z, AA-AD, 2004.|
|9||Dusseault et al, "Pressure Pulse Workovers in Heavy Oil", SPE 79033, 2002.|
|10||Felsenthal et al., Pressure Pulsing-An Improved Method of Waterflooding Fractured Reservoirs SPE 1788, 1957.|
|11||Foreign Search Report and Opinion (CPW 21582 EP).|
|12||Funkhouser et al., "Synthetic Polymer Fracturing Fluid For High-Temperature Applications", SPE 80236, 2003.|
|13||Gidley et al., "Recent Advances in Hydraulic Fracturing," Chapter 6, pp. 109-130, 1989.|
|14||Gorman, Plastic Electric: Lining up the Future of Conducting Polymers Science News, vol. 163, May 17, 2003.|
|15||Halliburton "CobraFrac<SUP>SM</SUP> Service, Coiled Turbing Fracturing-Cost-Effective Method for Stimulating Untapped Reserves", 2 pages, 2004.|
|16||Halliburton "CobraJetFrac<SUP>SM</SUP> Service, Cost-Effective Technology That Can Help Reduce Cost per BOE Produced, Shorten Cycle time and Reduce Capex", undated.|
|17||Halliburton "SurgiFrac<SUP>SM</SUP> Service, a Quick and cost-Effective Method to Help Boost Production From Openhole Horizonal Completions", 2002.|
|18||Halliburton brochure entitled "H2Zero(TM) Service Introducing The Next Generation of cost-Effective Conformance Control Solutions", 2002.|
|19||Halliburton brochure entitled "INJECTROL(R) G Sealant", 1999.|
|20||Halliburton brochure entitled "INJECTROL(R) IT Sealant", 1999.|
|21||Halliburton brochure entitled "INJECTROL(R) Service Treatment", 1999.|
|22||Halliburton brochure entitled "INJECTROL(R) U Sealant", 1999.|
|23||Halliburton brochure entitled "Pillar Frac Stimulation Technique" Fracturing Services Technical Data Sheet, 2 pages, undated.|
|24||Halliburton brochure entitled "Sanfix(R) A Resin", 1999.|
|25||Halliburton brochure entitled INJECTROL(R) A Component, 1999.|
|26||Halliburton Cobra Frac Advertisement, 2001.|
|27||Halliburton Technical Flier-Multi Stage Frac Completion Methods, 2 pages, undated.|
|28||Halliburton, CoalStim<SUP>SM</SUP> Service, Helps Boost Cash Flow From CBM Assets, Stimulation, HO3679 Oct. 2003, Halliburton Communications.|
|29||Halliburton, Conductivity Endurance Technology For High Permeability Resevoirs, Helps Prevent Intrusion of Formation Material Into the Proppant Pack for Improved Long-term Production, Stimulation, 2003, Halliburton Communications.|
|30||Halliburton, Expedite(R) Service, A Step-Change Improvement Over Conventional Proppant Flowback Control Systems. Provides Up to Three Times the Conductivity of RCPs., Stimulation, HO3296 May 2004, Halliburton Communications.|
|31||Halliburton, SandWedge(R) NT Conductivity Enhancement System, Enhances Proppant Pack Conductivity and Helps Prevent Intrusion of Formation Material for Improved Long-Term Production, Stimulation, HO2289 May 2004, Halliburton Communications.|
|32||Kazakov et al., "Optimizing and Managing Coiled Tubing Frac Strings" SPE 60747, 2000.|
|33||Love et al., "Selectively Placing Many Fractures in Openhole Horizontal Wells Improves Production", SPE 50422, 1998.|
|34||McDaniel et al. "Evolving New Stimulation Process Proves Highly Effective In Level 1 Dual-Lateral Completion" SPE 78697, 2002.|
|35||Nguyen et al., A Novel Approach For Enhancing Proppant Consolidation: Laboratory Testing And Field Applications, SPE Paper No. 77748, 2002.|
|36||Nguyen et al., New Guidelines For Applying Curable Resin-Coated Proppants, SPE Paper No. 39582, 1997.|
|37||Owens et al., Waterflood Pressure Pulsing for Fractured Reservoirs SPE 1123, 1966.|
|38||Peng et al., "Pressure Pulsing Waterflooding in Dual Porosity Naturally Fractured Reservoirs" SPE 17587, 1988.|
|39||Raza, "Water and Gas Cyclic Pulsing Method for Improved Oil Recovery", SPE 3005, 1971.|
|40||S. W. Almond, et al., "Factors Affecting Proppant Flowback With Resin Coated Proppants," Society of Petroleum Engineers, Inc., SPE 30096, pp. 171-186, 1995.|
|41||Simmons et al., "Poly(phenyllactide): Synthesis, Characterization, and Hydrolytic Degradation, Biomacromolecules", vol. 2, No. 2, pp. 658-663, 2001.|
|42||SPE 15547, Field Application of Lignosulfonate Gels To Reduce Channeling, South Swan Hills Miscible Unit, Alberta, Canada, by O.R. Wagner et al, 1986.|
|43||SPE 82215, Controlling Proppant Flowback in High-Temperature, High-Production Wells. Nguyen, P., Weaver, J., May 2003.|
|44||SPE 90398, Maximizing Effective Proppant Permeability under High-Stress, High Gas-Rate Conditions. Dusterhoft, R., Nguyen, P., Conway, M., Sep. 2004.|
|45||Vichaibun et al., "A New Assay for the Enzymatic Degradation of Polylactic Acid, Short Report", ScienceAsia, vol. 29, pp. 297-300, 2003.|
|46||Yang et al., "Experimental Study on Fracture Initiation By Pressure Pulse", SPE 63035, 2000.|
|47||Yin et al., "Preparation and Characterization of Substituted Polylactides", Americal Chemical Society, vol. 32, No. 23, pp. 7711-7718, 1999.|
|48||Yin et al., "Synthesis and Properties of Polymers Derived from Substituted Lactic Acids", American Chemical Society, Ch. 12, pp. 147-159, 2001.|
|49||Yoary Attia, et al.., "Adsorption Thermodynamics of a Hydrophobic Polymeric Flocculant on Hydrophobic Colloidal Coal Particulates," American Chemical Society, p. 2203-2207, 1991.|
|Patente citante||Fecha de presentación||Fecha de publicación||Solicitante||Título|
|US7673686||10 Feb 2006||9 Mar 2010||Halliburton Energy Services, Inc.||Method of stabilizing unconsolidated formation for sand control|
|US7712531||26 Jul 2007||11 May 2010||Halliburton Energy Services, Inc.||Methods for controlling particulate migration|
|US7762329||27 Ene 2009||27 Jul 2010||Halliburton Energy Services, Inc.||Methods for servicing well bores with hardenable resin compositions|
|US7766099||23 Oct 2008||3 Ago 2010||Halliburton Energy Services, Inc.||Methods of drilling and consolidating subterranean formation particulates|
|US7788037||8 Ene 2005||31 Ago 2010||Halliburton Energy Services, Inc.||Method and system for determining formation properties based on fracture treatment|
|US7819192||10 Feb 2006||26 Oct 2010||Halliburton Energy Services, Inc.||Consolidating agent emulsions and associated methods|
|US7926591||12 Ene 2009||19 Abr 2011||Halliburton Energy Services, Inc.||Aqueous-based emulsified consolidating agents suitable for use in drill-in applications|
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|Clasificación de EE.UU.||166/280.2, 507/924, 507/219, 166/281, 166/295, 507/220|
|Clasificación cooperativa||E21B43/267, Y10S507/924, C09K8/68, C09K8/805, C09K8/685, C09K8/703|
|Clasificación europea||C09K8/80B, C09K8/68B, C09K8/70B, E21B43/267, C09K8/68|
|11 Feb 2005||AS||Assignment|
Owner name: HALLIBURTON ENERGY SERVICES, INC., TEXAS
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:DUSTERHOFT, RONALD G.;FITZPATRICK, HARVEY J.;ADAMS, DAVID;AND OTHERS;REEL/FRAME:016288/0318;SIGNING DATES FROM 20050208 TO 20050211
|24 Ago 2011||FPAY||Fee payment|
Year of fee payment: 4
|25 Ago 2015||FPAY||Fee payment|
Year of fee payment: 8